JPS6160359B2 - - Google Patents
Info
- Publication number
- JPS6160359B2 JPS6160359B2 JP14466281A JP14466281A JPS6160359B2 JP S6160359 B2 JPS6160359 B2 JP S6160359B2 JP 14466281 A JP14466281 A JP 14466281A JP 14466281 A JP14466281 A JP 14466281A JP S6160359 B2 JPS6160359 B2 JP S6160359B2
- Authority
- JP
- Japan
- Prior art keywords
- hopper
- ore
- auxiliary
- lumps
- auxiliary hopper
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000007789 gas Substances 0.000 claims description 30
- 230000001105 regulatory effect Effects 0.000 claims description 14
- 239000000112 cooling gas Substances 0.000 claims description 12
- 239000011261 inert gas Substances 0.000 claims description 7
- 239000000571 coke Substances 0.000 claims description 4
- 230000001276 controlling effect Effects 0.000 claims 1
- 238000001816 cooling Methods 0.000 description 6
- 238000007599 discharging Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000004200 deflagration Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
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- Furnace Details (AREA)
Description
【発明の詳細な説明】
本発明は高温の塊状物と冷却用ガスとの熱交換
等に使用される環状移動火格子式熱交換装置の改
良に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in an annular moving grate type heat exchange device used for heat exchange between a hot mass and a cooling gas.
一般に、この種熱交換装置の構成は、第1図及
び第2図に示すように外気と遮断された環状の空
間内を走行する多数のパレツトTを連設してなる
環状の移動火格子1上に、赤熱状のコークス等高
温の塊状物2を給鉱ホツパー3から一定の層厚に
積載し、前記環状の空間内にガスシール機構4を
もつて数室に分割された冷却室5a,5b,5c
内を順次移行する。分割された各冷却室は夫々風
箱6とフード7を有し、各室はダクト8で直列に
接続されており、この中を冷却用ガス9が押込フ
アン10により前記塊状物温度の低い室から高い
室へ、且つ塊状物層の下から上へと横切つて流れ
るように構成されている。この冷却用ガス9は各
室で塊状物2と接触し受熱した後、廃熱ボイラ1
1に導かれて蒸気を発生させ、放熱して再び塊状
物2の冷却用ガス9として循環使用される。一方
冷却された塊状物2は排鉱部で前記火格子1上か
ら排鉱ホツパー12内に排出される。 In general, this type of heat exchange device has a structure as shown in FIGS. 1 and 2, in which an annular movable grate 1 is formed by connecting a large number of pallets T that run in an annular space cut off from the outside air. A cooling chamber 5a is loaded with high-temperature lumps 2 such as red-hot coke from the feed hopper 3 to a certain layer thickness, and is divided into several chambers with a gas sealing mechanism 4 in the annular space. 5b, 5c
The files will be migrated sequentially. Each of the divided cooling chambers has a wind box 6 and a hood 7, and each chamber is connected in series through a duct 8, through which cooling gas 9 is forced into the chamber where the temperature of the lumps is low. from the bottom to the higher chamber and across the agglomerate layer from the bottom to the top. After this cooling gas 9 comes into contact with the lumps 2 in each chamber and receives heat, the cooling gas 9 is sent to the waste heat boiler 1.
1 to generate steam, which radiates heat and is recycled and used again as a cooling gas 9 for the lumps 2. On the other hand, the cooled lumps 2 are discharged from the ore discharge section onto the grate 1 into the ore discharge hopper 12.
而して、環状移動火格子1の雰囲気圧は給鉱ホ
ツパー3部が高く、排鉱ホツパー12部が低い大
気圧以上のガスが存在し、且つ両者間に設けられ
た各冷却室5a,5b,5c内気圧は、ある一定
の圧力差を保持しながら順次冷却ガス9を直列的
に通過せしめている。ところが、斯かるガス流通
状態において、塊状物2を給鉱ホツパー3に装入
する際、または塊状物2を排鉱ホツパー12から
排出する際、これらホツパー3,12に付設して
いる蓋あるいはダンパー13a,13bを開放す
ると、給鉱部および排鉱部の雰囲気ガスが流出
し、あるいは空気が侵入する等の現象が生じ、圧
力の変動が起つて、この影響は順次各冷却室の気
圧に波及し、これら各室を通過するガス量に大き
な変動を惹起して、各室間のガスリーク量の増
大、不均一冷却、あるいは冷却効果の減退等の障
害を招来する重大な欠点があつた。 Therefore, the atmospheric pressure of the annular moving grate 1 is high in the 3 portions of the ore feed hopper and low in the 12 portions of the ore discharge hopper. , 5c, the cooling gas 9 is sequentially passed in series while maintaining a certain pressure difference. However, in such a gas flow state, when charging the lumps 2 into the ore feeding hopper 3 or discharging the lumps 2 from the ore discharge hopper 12, the lids or dampers attached to these hoppers 3 and 12 When 13a and 13b are opened, phenomena such as atmospheric gas flowing out of the ore feeding section and ore discharging section or air intrusion occur, causing pressure fluctuations, and this effect sequentially spreads to the air pressure in each cooling chamber. However, there was a serious drawback in that the amount of gas passing through each chamber varied greatly, leading to problems such as an increase in the amount of gas leaking between the chambers, uneven cooling, or a decrease in the cooling effect.
斯かる現象は、塊状物2の粒径が大きくなるに
従い、塊状物粒子間をガスが通過し易くなること
と相挨つて増大する傾向があつた。 This phenomenon tended to increase as the particle size of the agglomerates 2 became larger, as it became easier for gas to pass between the agglomerate particles.
更に、塊状物2が赤熱コークスの場合などに
は、冷却用ガス9内にCO等の可燃性ガス、有毒
ガスが生じ、これが大気中に放散し、あるいは装
置内に大気の侵入によつて爆燃あるいは消火不良
等の危険性が生ずるなどの欠点もあつた。 Furthermore, when the lumps 2 are red-hot coke, combustible gases such as CO or toxic gases are generated in the cooling gas 9, and this is dissipated into the atmosphere or deflagration occurs due to air entering the equipment. There were also drawbacks, such as the risk of inadequate extinguishing.
本発明は叙上の従来装置の欠点に鑑みて、移動
火格子雰囲気を形成する冷却用ガス系内の圧力、
流量を塊状物の装入、排出に関係なく一定に保持
し、装置の運転を安定化して運動効率を高め、且
つ操業の安全性を確保し得るこの種装置を提案す
るものである。 In view of the above-mentioned drawbacks of the conventional devices, the present invention aims to reduce the pressure in the cooling gas system forming the moving grate atmosphere.
The present invention proposes a device of this type that can maintain a constant flow rate regardless of the charging and discharging of lumps, stabilize the operation of the device, increase the efficiency of movement, and ensure operational safety.
而して、本発明の要旨とするところは、外気と
遮断された環状空間内を走行する多数のパレツト
を連設してなる環状の移動火格子上に、赤熱状の
コークス等高温の塊状物を給鉱ホツパーから一定
の層厚に積載し、該層を横切る冷却用ガスによつ
て冷却された前記塊状物を排鉱ホツパーから排出
するようにした環状移動火格子式熱交換装置にお
いて、前記給鉱ホツパーおよび排鉱ホツパー夫々
に、前記塊状物を一時貯溜するための補助ホツパ
ーを付設すると共に、該補助ホツパーの塊状物の
装入口および取出口に夫々気密のダンパーを設
け、且つ、上記給鉱ホツパーに付設された補助ホ
ツパーと不活性ガス供給源とを結ぶ配管系に設け
られて第1の調整弁、同補助ホツパーと排ガス処
理装置とを結ぶ配管系に設けられた第2の調整
弁、同補助ホツパー内圧力と給鉱ホツパー内圧力
とを検出し上記第1および第2の調整弁をコント
ロールする第1のガス圧調整器、上記排鉱ホツパ
ーに付設された補助ホツパーと不活性ガス供給源
とを結ぶ配管系に設けられた第3の調整弁、同補
助ホツパーと排ガス処理装置とを結ぶ配管系に設
けられた第4の調整弁、同補助ホツパー内圧力と
排鉱ホツパー内圧力とを検出し、上記第3および
第4の調整弁をコントロールする第2のガス圧調
整器を具備せしめたことを特徴とする環状移動火
格子式熱交換装置に在る。 The gist of the present invention is that hot lumps such as red-hot coke are placed on an annular moving grate made up of a number of consecutive pallets that run in an annular space that is cut off from the outside air. In the annular moving grate type heat exchange device, wherein the ore is loaded in a constant layer thickness from the ore feed hopper, and the agglomerates cooled by the cooling gas that crosses the layer are discharged from the ore discharge hopper. An auxiliary hopper for temporarily storing the agglomerates is attached to each of the ore feed hopper and the ore discharge hopper, and airtight dampers are provided at the agglomerate loading and unloading ports of the auxiliary hoppers, respectively. A first regulating valve provided in a piping system connecting an auxiliary hopper attached to the ore hopper and an inert gas supply source, and a second regulating valve provided in a piping system connecting the auxiliary hopper and the exhaust gas treatment device. , a first gas pressure regulator that detects the internal pressure of the auxiliary hopper and the internal pressure of the ore feed hopper and controls the first and second regulating valves; an auxiliary hopper attached to the ore discharge hopper and an inert gas; A third regulating valve provided in the piping system connecting the supply source, a fourth regulating valve provided in the piping system connecting the auxiliary hopper and the exhaust gas treatment device, the internal pressure of the auxiliary hopper, and the internal pressure of the ore discharge hopper. The annular moving grate type heat exchange device is characterized in that it is equipped with a second gas pressure regulator that detects and controls the third and fourth regulating valves.
さて本発明装置の構成は、給鉱部および排鉱部
に特徴を有し、その他の構成は第1図および第2
図に示した従来装置の構成と同様であるので、説
明並びに詳細な図示を省略することとする。 Now, the configuration of the device of the present invention is characterized by an ore feeding section and an ore discharge section, and the other configurations are shown in Figs. 1 and 2.
Since the configuration is the same as that of the conventional device shown in the figure, explanation and detailed illustration will be omitted.
第3図において示す本発明装置の給鉱部は、給
鉱ホツパー3の上流に塊状物2の装入口と取出口
夫々にダンパー13cと13aを有する補助ホツ
パー14が一体的且つ気密に接続されており、同
様に、排鉱部には、排鉱ホツパー12の下流に塊
状物2の装入口と取出口夫々にダンパー13b,
13dを有する補助ホツパー15が設けられてい
る。又補助ホツパー14,15には夫々連設され
た給鉱ホツパー3と排鉱ホツパー12内の圧力と
均圧ならしめるためのN2ガス等の不活性ガス源
Bと、同補助ホツパー14,15内のガス例えば
CO等の有害あるいは可燃性ガスを吸引し、ガス
処理装置Cとを結ぶフアンおよび調整弁Vを有す
る配管系で結ばれている。 In the ore feeding section of the apparatus of the present invention shown in FIG. 3, an auxiliary hopper 14 having dampers 13c and 13a at the loading and unloading ports of the lumps 2 is integrally and airtightly connected upstream of the ore feeding hopper 3. Similarly, in the ore discharge section, dampers 13b are provided downstream of the ore discharge hopper 12 at the charging and unloading ports of the lumps 2, respectively.
An auxiliary hopper 15 having a diameter 13d is provided. The auxiliary hoppers 14 and 15 also have an inert gas source B such as N 2 gas for equalizing the pressure in the ore feed hopper 3 and the ore discharge hopper 12 which are connected to each other, and the auxiliary hoppers 14 and 15. For example, gas in
It sucks in harmful or flammable gases such as CO and is connected to a gas treatment device C by a piping system having a fan and a regulating valve V.
而して、前記調整弁Vは給排鉱ホツパー3,1
2の圧力P1,P3とこれに付設された補助ホツパー
14,15夫々の圧力P2,P4を検出して両者が均
圧(P1=P2、P3=P4)になるよう指令を発するガ
ス圧調整器16,17によつて作動せしめられ、
その開度が自動的に調整される。 The regulating valve V is connected to the supply and discharge ore hoppers 3 and 1.
2 pressures P 1 and P 3 and the pressures P 2 and P 4 of the auxiliary hoppers 14 and 15 attached thereto are detected, and both become equal pressures (P 1 = P 2 , P 3 = P 4 ). operated by gas pressure regulators 16 and 17 which issue commands to
Its opening degree is automatically adjusted.
本発明において、前記給排鉱ホツパー3,12
内圧力を検出し、夫々の補助ホツパー14,15
内圧力をこれと均圧ならしめる前記ガス圧調整系
を総称して、ガス圧調整手段と呼称する。 In the present invention, the ore supply and discharge hopper 3, 12
The internal pressure is detected and each auxiliary hopper 14, 15
The gas pressure adjustment system that equalizes the internal pressure is collectively referred to as gas pressure adjustment means.
さて、本装置への塊状物2の装入操作につき述
べると、図示せざる運搬具により運搬されて来た
高温の塊状物2は補助ホツパー14に投入され
る。この際、装入口のダンパー13cは開、取出
口のダンパー13aは閉の状態にある。装入を終
れば、該装入口のダンパー13cを閉じ、補助ホ
ツパー14を密閉状態とする。然る後、給鉱ホツ
パー2内圧力P1と補助ホツパー14内圧力P2を均
圧あるいは後者の圧圧力P2を前者の圧力P1より両
ホツパー3,14の設置位置の高さの差によるド
ラフト分たけ高くなるよう前記ガス圧調整手段に
より圧力を調整した後、補助ホツパー14の取出
口ダンパー13aを開放して、補助ホツパー14
内に一時貯溜した塊状物2を給鉱ホツパー3内に
投下する。尚、補助ホツパー14内への大気の侵
入を防止する必要がある場合は、同ホツパー14
内に塊状物2を受け入れた後、装入口のダンパー
13cを閉じて同ホツパー14を密閉状態とな
し、前記不活性ガス源Bとガス処理装置Cのガス
系を作動させて同ホツパー14内の空気を含むガ
スを先づパージした後、前述の方法で給鉱ホツパ
ー3と補助ホツパー14内圧力の均圧操作と塊状
物2の装入移送操作を行えばよい。排鉱部におけ
る排鉱ホツパー12と補助ホツパー15による排
鉱操作も給鉱部における操作と同様にして、両ホ
ツパー12,15内の圧力を均等化させたのち、
一担排鉱ホツパー12内の塊状物2を補助ホツパ
ー15内に移動させ、上部のダンパー13bを閉
じて外気の侵入あるいは冷却用ガスの漏出を断つ
た後、下部のダンパー13dを開放して大気中に
塊状物を取り出す操作を行う。 Now, to describe the operation of charging the lumps 2 into the present apparatus, the high-temperature lumps 2 that have been transported by a carrier (not shown) are charged into the auxiliary hopper 14. At this time, the damper 13c at the loading port is open, and the damper 13a at the unloading port is closed. When charging is completed, the damper 13c of the charging port is closed, and the auxiliary hopper 14 is brought into a sealed state. After that, the pressure P 1 inside the feed hopper 2 and the pressure P 2 inside the auxiliary hopper 14 are equalized, or the pressure P 2 of the latter is determined from the pressure P 1 of the former by the difference in height between the installation positions of both hoppers 3 and 14. After adjusting the pressure by the gas pressure adjusting means so that the pressure is increased by the amount of the draft, the outlet damper 13a of the auxiliary hopper 14 is opened, and the
The lumps 2 temporarily stored therein are dropped into the ore feed hopper 3. In addition, if it is necessary to prevent atmospheric air from entering the auxiliary hopper 14,
After receiving the lumps 2 into the hopper 14, the damper 13c at the charging port is closed to seal the hopper 14, and the inert gas source B and the gas system of the gas treatment device C are activated to remove the hopper 14. After first purging the gas containing air, the pressure equalization operation of the internal pressures of the ore feed hopper 3 and the auxiliary hopper 14 and the operation of charging and transferring the lumps 2 may be carried out in the manner described above. The ore discharge operation using the ore discharge hopper 12 and the auxiliary hopper 15 in the ore discharge section is performed in the same manner as the operation in the ore supply section, and after equalizing the pressure in both hoppers 12 and 15,
The lumps 2 in the first ore discharge hopper 12 are moved into the auxiliary hopper 15, the upper damper 13b is closed to cut off the intrusion of outside air or the leakage of cooling gas, and then the lower damper 13d is opened and the atmosphere Perform an operation to remove the lumps inside.
斯くすることにより、塊状物2の環状移動火格
子1上への装入あるいは排出操作は大気と遮断さ
れた状態で且つ雰囲気圧力の変動を生ずることな
く実施できるので、冷却用ガスの流通系路に外乱
を与えることなく、正常な運転状態を維持するこ
とが出来るのみならず、有害なガスの大気への放
散あるいは空気の侵入による危険を阻止する上で
極めて有効である。 By doing so, the operation of charging or discharging the lumps 2 onto the annular movable grate 1 can be carried out in a state where they are isolated from the atmosphere and without causing fluctuations in the atmospheric pressure, so that the cooling gas flow path can be Not only can normal operating conditions be maintained without causing any disturbance to the engine, but it is also extremely effective in preventing dangers due to the release of harmful gases into the atmosphere or the intrusion of air.
第1図は従来公知の環状移動火格子式熱交換装
置の説明図、第2図は第1図の線A部分で切断
し、これを展開した縦断面図、第3図は第2図に
相応する本発明装置の1実施例を示す縦断面図で
ある。
1……環状移動火格子、2……塊状物、3……
給鉱ホツパー、4……シール機構、5a,5b,
5c……冷却室、12……排鉱ホツパー、13
a,13b,13c,13d……ダンパー、1
4,15……補助ホツパー、B……不活性ガス
源、C……有害ガス処理装置、P1〜P5……各部の
ガス圧、T……パレツト、V……ガス調節弁。
Fig. 1 is an explanatory diagram of a conventionally known annular moving grate type heat exchange device, Fig. 2 is a vertical sectional view taken along line A in Fig. 1 and developed, and Fig. 3 is the same as Fig. 2. 1 is a longitudinal sectional view of a corresponding embodiment of the device according to the invention; FIG. 1... annular moving grate, 2... lumps, 3...
Ore feeding hopper, 4...Seal mechanism, 5a, 5b,
5c... Cooling room, 12... Ore hopper, 13
a, 13b, 13c, 13d...damper, 1
4,15...Auxiliary hopper, B...Inert gas source, C...Harmful gas treatment device, P1 to P5 ...Gas pressure at each part, T...Pallet, V...Gas control valve.
Claims (1)
のパレツトを連設してなる環状の移動火格子上
に、赤熱状コークス等高温の塊状物を給鉱ホツパ
ーから一定の層厚に積載し、該層を横切る冷却用
ガスによつて冷却された前記塊状物を排鉱ホツパ
ーから排出するようにした環状移動火格子式熱交
換装置において、前記給鉱ホツパーおよび排鉱ホ
ツパー夫々に、前記塊状物を一時貯溜するための
補助ホツパーを付設すると共に、該補助ホツパー
の塊状物の装入口および取出口に夫々気密のダン
パーを設け、且つ、上記給鉱ホツパーに付設され
た補助ホツパーと不活性ガス供給源とを結ぶ配管
系に設けられた第1の調整弁、同補助ホツパーと
排ガス処理装置とを結ぶ配管系に設けられた第2
の調整弁、同補助ホツパー内圧力と給鉱ホツパー
内圧力とを検出し上記第1および第2の調整弁を
コントロールする第1のガス圧調整器、上記排鉱
ホツパーに付設された補助ホツパーと不活性ガス
供給源とを結ぶ配管系に設けられた第3の調整
弁、同補助ホツパーと排ガス処理装置とを結ぶ配
管系に設けられた第4の調整弁、同補助ホツパー
内圧力と排鉱ホツパー内圧力とを検出し、上記第
3および第4の調整弁をコントロールする第2の
ガス圧調整器を具備せしめたことを特徴とする環
状移動火格子式熱交換装置。1. High-temperature lumps such as red-hot coke are loaded from the feed hopper to a certain layer thickness onto a moving annular grate made up of a number of pallets that run in an annular space cut off from the outside air. In the annular moving grate type heat exchange device, the lumps cooled by the cooling gas that crosses the layer are discharged from the ore hopper, and the lumps are discharged into each of the feed hopper and the discharge hopper. An auxiliary hopper is attached to temporarily store the ore, and an airtight damper is provided at each of the lump loading and unloading ports of the auxiliary hopper, and the auxiliary hopper attached to the feeding hopper and the inert gas supply The first regulating valve is installed in the piping system connecting the source, and the second regulating valve is installed in the piping system connecting the auxiliary hopper and the exhaust gas treatment device.
a first gas pressure regulator that detects the internal pressure of the auxiliary hopper and the internal pressure of the ore feed hopper and controls the first and second regulating valves, an auxiliary hopper attached to the ore discharge hopper; A third regulating valve installed in the piping system connecting the inert gas supply source, a fourth regulating valve installed in the piping system connecting the auxiliary hopper and the exhaust gas treatment device, and controlling the internal pressure of the auxiliary hopper and the discharged ore. 1. An annular moving grate type heat exchange device, comprising a second gas pressure regulator that detects the internal pressure of the hopper and controls the third and fourth regulating valves.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14466281A JPS5847984A (en) | 1981-09-16 | 1981-09-16 | Annular moving grate type heat exchanging device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14466281A JPS5847984A (en) | 1981-09-16 | 1981-09-16 | Annular moving grate type heat exchanging device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5847984A JPS5847984A (en) | 1983-03-19 |
| JPS6160359B2 true JPS6160359B2 (en) | 1986-12-20 |
Family
ID=15367301
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14466281A Granted JPS5847984A (en) | 1981-09-16 | 1981-09-16 | Annular moving grate type heat exchanging device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5847984A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5534120A (en) * | 1995-07-03 | 1996-07-09 | Toto Ltd. | Membraneless water electrolyzer |
-
1981
- 1981-09-16 JP JP14466281A patent/JPS5847984A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5847984A (en) | 1983-03-19 |
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